US4405603A - Method for rendering factors IX and X hepatitis-safe with calcium ions - Google Patents

Method for rendering factors IX and X hepatitis-safe with calcium ions Download PDF

Info

Publication number
US4405603A
US4405603A US06/324,872 US32487281A US4405603A US 4405603 A US4405603 A US 4405603A US 32487281 A US32487281 A US 32487281A US 4405603 A US4405603 A US 4405603A
Authority
US
United States
Prior art keywords
hepatitis
factor
safe
calcium ions
factors
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US06/324,872
Inventor
Horst Schwinn
Norbert Heimburger
Gerhardt Kumpe
Wilfried Wormsbacher
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Centeon Pharma GmbH
Original Assignee
Behringwerke AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Behringwerke AG filed Critical Behringwerke AG
Assigned to BEHRINGWERKE AKTIENGESELLSCHAFT reassignment BEHRINGWERKE AKTIENGESELLSCHAFT ASSIGNMENT OF ASSIGNORS INTEREST. Assignors: HEIMBURGER, NORBERT, KUMPE, GERHARDT, SCHWINN, HORST, WORMSBACHER, WILFRIED
Application granted granted Critical
Publication of US4405603A publication Critical patent/US4405603A/en
Assigned to HOECHST AKTIENGESELLSCHAFT reassignment HOECHST AKTIENGESELLSCHAFT MERGER (SEE DOCUMENT FOR DETAILS). Assignors: BERHINGWERKE GMBH
Assigned to CENTEON PHARMA GMBH reassignment CENTEON PHARMA GMBH ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: HOECHST AKTIENGESELLSCHAFT
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes
    • C12N9/14Hydrolases (3)
    • C12N9/48Hydrolases (3) acting on peptide bonds (3.4)
    • C12N9/50Proteinases, e.g. Endopeptidases (3.4.21-3.4.25)
    • C12N9/64Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue
    • C12N9/6421Proteinases, e.g. Endopeptidases (3.4.21-3.4.25) derived from animal tissue from mammals
    • C12N9/6424Serine endopeptidases (3.4.21)
    • C12N9/647Blood coagulation factors not provided for in a preceding group or according to more than one of the proceeding groups
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K35/00Medicinal preparations containing materials or reaction products thereof with undetermined constitution
    • A61K35/12Materials from mammals; Compositions comprising non-specified tissues or cells; Compositions comprising non-embryonic stem cells; Genetically modified cells
    • A61K35/14Blood; Artificial blood
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/0005Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor for pharmaceuticals, biologicals or living parts
    • A61L2/0011Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor for pharmaceuticals, biologicals or living parts using physical methods
    • A61L2/0023Heat
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61LMETHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/04Heat
    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K38/00Medicinal preparations containing peptides

Definitions

  • the invention relates to a process for the production of a virtually hepatitis-safe preparation of the blood-clotting Factors IX and X by warming in the presence of calcium ions, if appropriate in the additional presence of an amino acid and/or a saccharide or sugar alcohol.
  • Blood-clotting is a complex function which proceeds in stages and is initiated by various physiological as well as pathological causes and the course of which depends on about 20 promoting and inhibiting factors. As a result of a reduction or increase in these blood-clotting factors, disorders of blood-clotting arise and some of these manifest themselves as diseases.
  • Factor IX and X-containing preparations which are useful for treating disturbances as caused by deficiencies of these factors, are known.
  • Albumin is regarded as hepatitis-safe, if it is heated in aqueous solution at 60° C., in the presence of stabilizers (Gellis, S.S. et al., J. Clin. Invest. (1948) 27, 239). It may therefore be assumed that a Factor IX and/or X concentrate which has been heated in the presence of suitable stabilizers is also hepatitis-safe.
  • German Offenlegungsschrift No. 2,916,711 has disclosed a process for the heat-stabilization of other clotting factors in aqueous solution by adding an aminoacid and a monosaccharide or oligosaccharide or a sugar alcohol.
  • the invention relates to a process for the production of a virtually hepatitis-safe preparation of blood-clotting Factors IX and/or X by warming in the presence of calcium ions, if appropriate in the additional presence of an aminoacid and/or a saccharide or sugar alcohol.
  • the calcium ions are added in a concentration of from 0.05 to 2.0, preferably 0.4 to 0.6, moles/l.
  • calcium nitrate as well as any water-soluble calcium salts of saccharic acids such as gluconic acid, lactonic acid etc.
  • CaCl 2 and Ca(Ac) 2 are preferably used.
  • the aqueous solution of the clotting factors can be heated for such a long period that, according to the present state of knowledge, the transmission of hepatitis pathogens can be virtually excluded.
  • a preparation which has been kept for at least 10 hours at about 60° C. in aqueous solution is nowadays regarded as virtually hepatitis-safe, in particular if the starting material used is human tissue in which hepatitis viruses cannot be detected by means of a test of the third generation.
  • 0.05 to 2.0 moles/l of one of the soluble calcium salts preferably 0.4 to 0.6 mole/l of CaCl 2 and, if appropriate, 1.0 to 3.0 moles/l of at least one of the aminoacids glycine, ⁇ - or ⁇ -alanine, hydroxyproline, proline, glutamine or ⁇ -, ⁇ - or ⁇ -aminobutyric acid, preferably glycine, and 20 to 60% by weight of monosaccharides or oligosaccharides or sugar alcohols, preferably 1.0 to 3.0 moles/l of glycine and 20 to 60% by weight of sucrose, are added to a solution containing Factor IX and/or Factor X, preferably a plasma fraction or placenta fraction, the mixture is heated to a temperature of between 30° C.
  • Factor IX and/or Factor X preferably a plasma fraction or placenta fraction
  • the pH value must be matched specifically to the individual clotting factors present in the solution. In general, a pH value within the limits of 6.5 and 8.0 should be maintained. A virtually hepatitis-safe preparation of Factor IX and/or Factor X is obtained.
  • the values of 0.3 and 3.0 moles/l or 60% by weight respectively can be extended to higher concentrations, if the calcium salt, the aminoacid or the carbohydrate have a correspondingly higher solubility at the desired temperature.
  • the heat treatment can also be carried out in several successive steps.
  • a hepatitis-safe preparation is obtained by heating under the following condition: heating for 10 to 20 hours at 60° to 70° C. in the presence of CaCl 2 in a concentration from 0.4 to 0.6 moles/l, sucrose in a concentration from 40 to 60% by weight and of glycine in a concentration from 1.0 to 2.5 moles/l, at a pH value from 6.8 to 8.0.
  • the recovery and purification of the clotting factors from the heated solution can be carried out by precipitation with 30-45% weight/volume of ammonium sulfate and adsorption of the supernatant liquid on 0.4 to 1.0% weight/volume of Ca phosphate.
  • the starting fractions are those in which the factor to be stabilized has been enriched according to the cited process.
  • the starting material used is a fraction such as is obtained, for example, by the process of Soulier et al., Thrombosis Diath. Haemorrh. Suppl. 35, 61 (1969).
  • plasma obtained from blood anti-coagulated with 0.01 mole/l of EDTA is adsorbed on Ca phosphate, and the solid is centrifuged off.
  • the factors are quantitatively bound to the adsorbent and can be recovered by several elutions with 0.2 mole/l of trisodium citrate.
  • the combined eluates are further purified by combined alcohol and acetic acid precipitations at temperatures from -8° C. to +4° C. At the same time, the factors are thus concentrated.
  • the concentrate is taken up at a pH of 7.5 in a suitable buffer, preferably sodium chloride/sodium citrate in concentrations of 0.06 and 0.02 mole/l respectively.
  • One part for example 0.1 ml of partial thromboplastin, for example as prepared according to German Auslegeschrift No. 2,316,430, one part of plasma deficient in Factor IX, and one part of diluted normal plasma are mixed. This mixture is kept for 36 minutes at +37° C. Subsequently, one part of a 0.025 molar calcium chloride solution preheated to 37° C. is added and the time is determined which elapses until a clot appears. For quantitative data, the clotting time resulting with the solution containing Factor IX is read off by reference to a calibration curve obtained with a dilution series of normal plasma.
  • IU International unit of Factor IX corresponds to the Factor IX activity of 1 ml of normal plasma.
  • Factor X can be determined, for example, by the method of Duckert, F. et al., Blood Coagulation, Hemorrhage and Thrombosis, Ed. Tocantins, L.M. and Kazal, L.A. (1964). For this purpose, one part, for example 0.1 ml of plasma deficient in Factor X, and one part of diluted normal plasma are mixed. This mixture is kept for 30 seconds at +37° C. Subsequently, two parts of calcium-containing thromboplastin prepared, for example, according to German Patent 2,356,493 are added and the time is determined which elapses until a clot appears. For quantitative data, the clotting time resulting with the solution containing Factor X is read off by reference to a calibration curve obtained with a dilution series of normal plasma.
  • Factor X corresponds to the Factor X activity of 1 ml of normal plasma.
  • the heated solution is centrifuged if necessary, and impurities are removed by precipitation with 30-45% weight/volume of ammonium sulfate.
  • the supernatant liquid is adsorbed on 0.04 to 1.0% weight/volume of calcium phosphate, the charged adsorbent is washed and eluted with citrate buffer, and the eluate is dialysed.
  • the product is subjected to sterilization by filtration.
  • the invention particularly relates to a hepatitis-safe preparation of Factors IX and/or X, which is obtained by this process.
  • protein-stabilizing substances for example proteins, aminoacids or carbohydrates
  • the preparation which has been subjected to this treatment can be made available in a freeze-dried form, and in this case an addition of anti-coagulants, such as, for example, heparin, can be advantageous.
  • the product according to the invention is a medicament for the treatment of coagulopathy, and it can be used intravenously, advantageously as an infusion, for the therapy and prophylaxis of hemorrhages caused by deficiencies in Factor IX and/or Factor X.
  • the absorbent is eluted with 7.5 liters of 1 mole/l NaCl solution at pH 8.0 and is then discarded.
  • 1.2 kg of glycine, 11.2 kg of sucrose and 0.55 kg of CaCl 2 .2H 2 O are added to the eluate, and the mixture is heated for 10 hours at 60° C. at pH 7.6.
  • the mixture is diluted with 50 liters of distilled water and brought to an ammonium sulfate concentration of 40% weight/volume.
  • the precipitate is centrifuged off and discarded.
  • 0.5 kg of Ca phosphate are added to the supernatant liquid which is left to stand for 30 minutes at pH 7.6.
  • the adsorbent is washed with two 10 liter portions of 0.5 mole/l NaCl solution.
  • the adsorbent is eluted with 1.8 liters of buffer of pH 8.0, which contains 0.2 mole/l of trisodium citrate, 0.15 mole/l of NaCl, 2 g/ 100 ml of glycine, 0.3 U/ml of antithrombin III and 14 IU/ml of heparin.
  • the eluate is separated from the adsorbent by centrifuging at 30,000 g.
  • the residue is discarded and the supernatant liquid is dialyzed for 3 hours against 100 liters of a buffer of pH 7, containing 0.06 mole/l of NaCl, 0.02 mole/l of trisodium citrate and 2 g/100 ml of glycine.
  • the dialyzate is tested for the activity of Factors IX and X, adjusted to the desired concentration, sterilized by filtration, divided into unit doses and lyophilized.
  • the lyophilized product from 4 dosage units of prothrombin complex concentrate, each having about 200 units, is taken up in 20 ml of an aqueous solution which contains 2.2 moles/l of glycine, 1 g/ml of sucrose and 0.5 mole/l of calcium chloride.
  • the pH value is 7.6.
  • the container is sealed airtight and incubated for 10 hours at 60° C. in a water bath.
  • the mixture is diluted with 160 ml of distilled water and brought to saturation with 40% weight/volume of ammonium sulfate.
  • the precipitate is centrifuged off and the supernatant liquid is adsorbed on 0.8 g of Ca phosphate.

Landscapes

  • Health & Medical Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biomedical Technology (AREA)
  • General Health & Medical Sciences (AREA)
  • Zoology (AREA)
  • Medicinal Chemistry (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Epidemiology (AREA)
  • Animal Behavior & Ethology (AREA)
  • Biotechnology (AREA)
  • Molecular Biology (AREA)
  • Hematology (AREA)
  • Organic Chemistry (AREA)
  • Wood Science & Technology (AREA)
  • Genetics & Genomics (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Cell Biology (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Immunology (AREA)
  • Microbiology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • Developmental Biology & Embryology (AREA)
  • Virology (AREA)
  • Medicines Containing Material From Animals Or Micro-Organisms (AREA)
  • Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
  • Peptides Or Proteins (AREA)
  • Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
  • Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)

Abstract

What is disclosed is a method for making a preparation containing blood clotting Factors IX and/or X virtually hepatitis-safe by warming said peparation in the presence of calcium ions and in the further presence of an amino acid and/or a saccharide or sugar alcohol.

Description

The invention relates to a process for the production of a virtually hepatitis-safe preparation of the blood-clotting Factors IX and X by warming in the presence of calcium ions, if appropriate in the additional presence of an amino acid and/or a saccharide or sugar alcohol.
Blood-clotting is a complex function which proceeds in stages and is initiated by various physiological as well as pathological causes and the course of which depends on about 20 promoting and inhibiting factors. As a result of a reduction or increase in these blood-clotting factors, disorders of blood-clotting arise and some of these manifest themselves as diseases.
Factor IX and X-containing preparations, which are useful for treating disturbances as caused by deficiencies of these factors, are known.
These preparations are not free from the risk of transmitting hepatitis.
Albumin is regarded as hepatitis-safe, if it is heated in aqueous solution at 60° C., in the presence of stabilizers (Gellis, S.S. et al., J. Clin. Invest. (1948) 27, 239). It may therefore be assumed that a Factor IX and/or X concentrate which has been heated in the presence of suitable stabilizers is also hepatitis-safe.
German Offenlegungsschrift No. 2,916,711 has disclosed a process for the heat-stabilization of other clotting factors in aqueous solution by adding an aminoacid and a monosaccharide or oligosaccharide or a sugar alcohol.
However, a complete inactivation of the Factors IX and X, when proceeding in the above manner, cannot be avoided.
Thus, there was still the object of discovering a process for the heat-stabilization of aqueous solutions of Factor IX and/or X concentrates, in order to reduce the losses in activity.
Surprisingly, it has now been found that an aqueous solution of Factor IX and/or Factor X can be heat-stabilized by the addition of calcium ions. Hitherto, no process for the stabilization of these factors against inactivation by heat was known.
The invention relates to a process for the production of a virtually hepatitis-safe preparation of blood-clotting Factors IX and/or X by warming in the presence of calcium ions, if appropriate in the additional presence of an aminoacid and/or a saccharide or sugar alcohol.
The calcium ions are added in a concentration of from 0.05 to 2.0, preferably 0.4 to 0.6, moles/l.
Examples of suitable salts donating calcium ion are:
calcium chloride (CaCl2),
calcium acetate (Ca(Ac)2),
calcium nitrate, as well as any water-soluble calcium salts of saccharic acids such as gluconic acid, lactonic acid etc.
CaCl2 and Ca(Ac)2 are preferably used.
In the presence of calicum ions of this type, the aqueous solution of the clotting factors can be heated for such a long period that, according to the present state of knowledge, the transmission of hepatitis pathogens can be virtually excluded. This applies especially in conjunction with precipitation processes in which the active ingredient remains in the supernatant liquid and the hepatitis viruses can be separated off together with the insoluble precipitate. A preparation which has been kept for at least 10 hours at about 60° C. in aqueous solution is nowadays regarded as virtually hepatitis-safe, in particular if the starting material used is human tissue in which hepatitis viruses cannot be detected by means of a test of the third generation.
In a particularly preferred embodiment of the invention, 0.05 to 2.0 moles/l of one of the soluble calcium salts, preferably 0.4 to 0.6 mole/l of CaCl2 and, if appropriate, 1.0 to 3.0 moles/l of at least one of the aminoacids glycine, α- or β-alanine, hydroxyproline, proline, glutamine or α-, β- or γ-aminobutyric acid, preferably glycine, and 20 to 60% by weight of monosaccharides or oligosaccharides or sugar alcohols, preferably 1.0 to 3.0 moles/l of glycine and 20 to 60% by weight of sucrose, are added to a solution containing Factor IX and/or Factor X, preferably a plasma fraction or placenta fraction, the mixture is heated to a temperature of between 30° C. and 100° C., preferably 60° C. to 100° C., and held at this temperature for 1 minute to 48 hours, preferably about 10 hours, the shortest time being associated with the highest temperature, and vice versa. To obtain a maximum yield, the pH value must be matched specifically to the individual clotting factors present in the solution. In general, a pH value within the limits of 6.5 and 8.0 should be maintained. A virtually hepatitis-safe preparation of Factor IX and/or Factor X is obtained.
Depending on the solubility of the calcium salt, the aminoacid or the carbohydrate, the values of 0.3 and 3.0 moles/l or 60% by weight respectively can be extended to higher concentrations, if the calcium salt, the aminoacid or the carbohydrate have a correspondingly higher solubility at the desired temperature. The heat treatment can also be carried out in several successive steps.
When the preferred combination of CaCl2 with glycine and sucrose is used, a hepatitis-safe preparation is obtained by heating under the following condition: heating for 10 to 20 hours at 60° to 70° C. in the presence of CaCl2 in a concentration from 0.4 to 0.6 moles/l, sucrose in a concentration from 40 to 60% by weight and of glycine in a concentration from 1.0 to 2.5 moles/l, at a pH value from 6.8 to 8.0.
As can be seen in the Table, Factors IX and X are stabilized against the action of heat by calcium ions.
              TABLE                                                       
______________________________________                                    
Effect of calcium ions on the stability of the clotting factors           
             Clotting factor                                              
             (U/ml)                                                       
             IX         X                                                 
               Before  After    Before                                    
                                      After                               
Stabilizers    heating heating  heating                                   
                                      heating                             
______________________________________                                    
Sucrose 60% by weight                                                     
               50       0       40     0                                  
Glycine 2 moles/l                                                         
Ca.sup.2+  0.5 mole/l                                                     
               50      48       40    35                                  
Sucrose 60% by weight                                                     
Glycine 2 moles/l                                                         
______________________________________                                    
The recovery and purification of the clotting factors from the heated solution can be carried out by precipitation with 30-45% weight/volume of ammonium sulfate and adsorption of the supernatant liquid on 0.4 to 1.0% weight/volume of Ca phosphate.
Advantageously, the starting fractions are those in which the factor to be stabilized has been enriched according to the cited process.
Due to the knowledge of the methods for the determination of the substances concerned, those skilled in the art are familiar with monitoring the measures for the enrichment and purification of Factor IX or X. Using these monitoring methods, the process conditions can be controlled with regard to a satisfactory yield and a satisfactory purity of the product.
To obtain a hepatitis-safe concentrate of Factors IX and X, the starting material used is a fraction such as is obtained, for example, by the process of Soulier et al., Thrombosis Diath. Haemorrh. Suppl. 35, 61 (1969). For this purpose, plasma obtained from blood anti-coagulated with 0.01 mole/l of EDTA is adsorbed on Ca phosphate, and the solid is centrifuged off. Thus, the factors are quantitatively bound to the adsorbent and can be recovered by several elutions with 0.2 mole/l of trisodium citrate. The combined eluates are further purified by combined alcohol and acetic acid precipitations at temperatures from -8° C. to +4° C. At the same time, the factors are thus concentrated.
The concentrate is taken up at a pH of 7.5 in a suitable buffer, preferably sodium chloride/sodium citrate in concentrations of 0.06 and 0.02 mole/l respectively.
Those skilled in the art are familiar with the activity determinations.
For Factor IX, this can be carried out, for example, by the following process:
One part, for example 0.1 ml of partial thromboplastin, for example as prepared according to German Auslegeschrift No. 2,316,430, one part of plasma deficient in Factor IX, and one part of diluted normal plasma are mixed. This mixture is kept for 36 minutes at +37° C. Subsequently, one part of a 0.025 molar calcium chloride solution preheated to 37° C. is added and the time is determined which elapses until a clot appears. For quantitative data, the clotting time resulting with the solution containing Factor IX is read off by reference to a calibration curve obtained with a dilution series of normal plasma.
One international unit (IU) of Factor IX corresponds to the Factor IX activity of 1 ml of normal plasma.
Factor X can be determined, for example, by the method of Duckert, F. et al., Blood Coagulation, Hemorrhage and Thrombosis, Ed. Tocantins, L.M. and Kazal, L.A. (1964). For this purpose, one part, for example 0.1 ml of plasma deficient in Factor X, and one part of diluted normal plasma are mixed. This mixture is kept for 30 seconds at +37° C. Subsequently, two parts of calcium-containing thromboplastin prepared, for example, according to German Patent 2,356,493 are added and the time is determined which elapses until a clot appears. For quantitative data, the clotting time resulting with the solution containing Factor X is read off by reference to a calibration curve obtained with a dilution series of normal plasma.
One unit of Factor X corresponds to the Factor X activity of 1 ml of normal plasma.
To destroy the hepatitis viruses, calcium ions and glycine and sucrose are added to the solution and the whole is heated.
For further purification, the heated solution is centrifuged if necessary, and impurities are removed by precipitation with 30-45% weight/volume of ammonium sulfate.
The supernatant liquid is adsorbed on 0.04 to 1.0% weight/volume of calcium phosphate, the charged adsorbent is washed and eluted with citrate buffer, and the eluate is dialysed.
For administration to humans, the product is subjected to sterilization by filtration.
The invention particularly relates to a hepatitis-safe preparation of Factors IX and/or X, which is obtained by this process.
To increase the storage stability, it is advantageous to add protein-stabilizing substances, for example proteins, aminoacids or carbohydrates, to the preparation. Finally, the preparation which has been subjected to this treatment can be made available in a freeze-dried form, and in this case an addition of anti-coagulants, such as, for example, heparin, can be advantageous.
In a solution suitable for pharmaceutical administration, the product according to the invention is a medicament for the treatment of coagulopathy, and it can be used intravenously, advantageously as an infusion, for the therapy and prophylaxis of hemorrhages caused by deficiencies in Factor IX and/or Factor X.
The invention will be explained in more detail by the examples which follow:
EXAMPLE 1
Preparation of a hepatitis-safe concentrate of Factors IX/X from human citrate plasma:
250 g of an anion exchanger (Type A50 Sephadex-DEAE) are added to 500 liters to citrate plasma, and the mixture is stirred for 60 minutes. After sedimentation of the adsorbent, the supernatant plasma is siphoned off and the residue is washed with 20 liters of 0.85% strength NaCl solution.
The absorbent is eluted with 7.5 liters of 1 mole/l NaCl solution at pH 8.0 and is then discarded. 1.2 kg of glycine, 11.2 kg of sucrose and 0.55 kg of CaCl2.2H2 O are added to the eluate, and the mixture is heated for 10 hours at 60° C. at pH 7.6. After cooling, the mixture is diluted with 50 liters of distilled water and brought to an ammonium sulfate concentration of 40% weight/volume. The precipitate is centrifuged off and discarded. 0.5 kg of Ca phosphate are added to the supernatant liquid which is left to stand for 30 minutes at pH 7.6. After centrifuging, the supernatant liquid is discarded and the adsorbent is washed with two 10 liter portions of 0.5 mole/l NaCl solution. The adsorbent is eluted with 1.8 liters of buffer of pH 8.0, which contains 0.2 mole/l of trisodium citrate, 0.15 mole/l of NaCl, 2 g/ 100 ml of glycine, 0.3 U/ml of antithrombin III and 14 IU/ml of heparin. After the addition of 0.2 g/100 ml of colloidal silica as a centrifuging aid, the eluate is separated from the adsorbent by centrifuging at 30,000 g. The residue is discarded and the supernatant liquid is dialyzed for 3 hours against 100 liters of a buffer of pH 7, containing 0.06 mole/l of NaCl, 0.02 mole/l of trisodium citrate and 2 g/100 ml of glycine. The dialyzate is tested for the activity of Factors IX and X, adjusted to the desired concentration, sterilized by filtration, divided into unit doses and lyophilized.
About 250 dosage units, each of 200 units of Factor IX, are obtained from 500 liters of plasma.
EXAMPLE 2
Heating of a Factor IX complex concentrate, produced by the process of Soulier et al. [Thromb. Diath. Haemorrh., Suppl. 35, 61, 1969], for inactivating the hepatitis viruses:
The lyophilized product from 4 dosage units of prothrombin complex concentrate, each having about 200 units, is taken up in 20 ml of an aqueous solution which contains 2.2 moles/l of glycine, 1 g/ml of sucrose and 0.5 mole/l of calcium chloride. The pH value is 7.6. After complete dissolution, the container is sealed airtight and incubated for 10 hours at 60° C. in a water bath. After cooling, the mixture is diluted with 160 ml of distilled water and brought to saturation with 40% weight/volume of ammonium sulfate. The precipitate is centrifuged off and the supernatant liquid is adsorbed on 0.8 g of Ca phosphate.
All the further steps are carried out corresponding to Example 1, taking into account the quantitative ratios which are transferable.

Claims (3)

We claim:
1. A method for making a preparation containing at least one member selected from the group consisting of blood clotting Factor IX and blood clotting Factor X virtually hepatitis-safe, which method comprises warming said preparation in the presence of an effective amount of calcium ions and in the further presence of an effective amount of at least one member selected from the group consisting of amino acids, saccharides, and sugar alcohols.
2. A method as in claim 1 wherein calcium ions are present in said preparation at a concentration from 0.05 mole/liter to 2.0 moles/liter.
3. A method as in claim 2 wherein said warming is at a temperature from 30° C. to 100° C. for 1 minute to 48 hours in the additional presence of 1.0 mole/liter to 3.0 moles/liter of at least one amino acid selected from the group consisting of glycine, α-alanine, β-alanine, hydroxyproline, proline, glutamine, and α-, β-, and γ-aminobutyric acids, and of 20 to 60 percent by weight of a member selected from the group consisting of monosaccharides, oligosaccharides, and sugar alcohols.
US06/324,872 1980-11-29 1981-11-25 Method for rendering factors IX and X hepatitis-safe with calcium ions Expired - Lifetime US4405603A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19803045153 DE3045153A1 (en) 1980-11-29 1980-11-29 METHOD FOR THE PRODUCTION OF BLOOD COagulation FACTORS AND THE PREPARATION OF FACTORS IX AND X THEREFORE PRODUCED
DE3045153 1980-11-29

Publications (1)

Publication Number Publication Date
US4405603A true US4405603A (en) 1983-09-20

Family

ID=6117972

Family Applications (1)

Application Number Title Priority Date Filing Date
US06/324,872 Expired - Lifetime US4405603A (en) 1980-11-29 1981-11-25 Method for rendering factors IX and X hepatitis-safe with calcium ions

Country Status (10)

Country Link
US (1) US4405603A (en)
EP (1) EP0053338B1 (en)
JP (1) JPS57120524A (en)
AT (1) ATE11640T1 (en)
AU (1) AU544157B2 (en)
CA (1) CA1182047A (en)
DE (2) DE3045153A1 (en)
ES (1) ES507400A0 (en)
IL (1) IL64396A (en)
MX (1) MX6947E (en)

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4490361A (en) * 1983-12-02 1984-12-25 Alpha Therapeutic Corporation Virus inactivating heat treatment of plasma fractions
WO1985005273A1 (en) * 1984-05-18 1985-12-05 Purcell Robert H Utilizing a halohydrocarbon containing dissolved water to inactivate a lipid virus
US4562072A (en) * 1982-10-09 1985-12-31 Behringwerke Aktiengesellschaft Process for the pasteurization of antihemophilic cryoprecipitate (AHC) and antihemophilic cryoprecipitate prepared thereby
US4687664A (en) * 1983-05-02 1987-08-18 Immuno Aktiengesellschaft Fur Chemisch-Medizinische Produkte Method of inactivating reproducible pathogens
US4764369A (en) * 1983-07-14 1988-08-16 New York Blood Center Inc. Undenatured virus-free biologically active protein derivatives
US4820805A (en) * 1983-07-14 1989-04-11 New York Blood Center, Inc. Undenatured virus-free trialkyl phosphate treated biologically active protein derivatives
WO1989005652A1 (en) * 1987-12-21 1989-06-29 American National Red Cross Pure factor ix product
US4876241A (en) * 1987-05-22 1989-10-24 Armour Pharmaceutical Company Stabilization of biological and pharmaceutical products during thermal inactivation of viral and bacterial contaminants
US4960757A (en) * 1982-08-19 1990-10-02 Behringwerke Aktiengesellschaft Pasteurized human fibrinogen (HF), a process for its preparation, and its use
WO1992015324A1 (en) * 1991-03-01 1992-09-17 Rhone-Poulenc Rorer International (Holdings) Inc. Preparation of factor ix
US5171569A (en) * 1985-03-15 1992-12-15 National Research Development Corporation Factor IX preparations uncontaminated by plasma components or pox virus
US5410022A (en) * 1992-04-24 1995-04-25 Immuno Aktiengesellschaft Method of producing a factor VIII preparation
US5614493A (en) * 1993-06-18 1997-03-25 Immuno Ag Use of human protein C for prevention and treatment of depositions of thrombocytes
US5614405A (en) * 1991-06-20 1997-03-25 Immuno Aktiengesellschaft Method of determining the virus inactivation capacity of an inactivation treatment
US5639730A (en) * 1992-12-16 1997-06-17 Immuno Aktiengesellschaft Method of producing a virus-safe biological preparation
US5770700A (en) * 1996-01-25 1998-06-23 Genetics Institute, Inc. Liquid factor IX formulations
EP1010852A1 (en) 1998-12-15 2000-06-21 Schlegel BVBA Sealing gasket and method of making and inserting the same
US6346277B1 (en) * 1983-10-08 2002-02-12 Aventis Behring Gmbh Process for the pasteurization of plasma or concentrates of blood coagulation factors II, VII, IX and X
US6372716B1 (en) * 1994-04-26 2002-04-16 Genetics Institute, Inc. Formulations for factor IX

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4456590B2 (en) * 1981-11-02 1989-05-30 Heat treatment of lyphilized blood clotting factor viii concentrate
DE3330770A1 (en) * 1983-08-26 1985-03-14 Behringwerke Ag, 3550 Marburg METHOD FOR PASTEURIZING HUMAN PLASMA
JPS6094917A (en) * 1983-10-28 1985-05-28 Green Cross Corp:The Production of vaccine for preventing infection to hepatitis b
AT389815B (en) * 1984-03-09 1990-02-12 Immuno Ag METHOD FOR INACTIVATING VARIABLE FILTERABLE DISEASERS IN BLOOD PRODUCTS
AT390560B (en) * 1986-05-30 1990-05-25 Immuno Ag METHOD FOR INACTIVATING VARIABLE FILTERABLE DISEASES
IL86417A (en) * 1987-05-22 1992-09-06 Armour Pharma Process for the inactivation of pathogens in biological or pharmaceutical material by mixing with aqueous solution containing a sugar(alcohol)and neutral salts as stabilizers
DE4001451A1 (en) * 1990-01-19 1991-08-01 Octapharma Ag STABLE INJECTABLE SOLUTIONS OF FACTOR VIII AND FACTOR IX
FR2664165B1 (en) * 1990-07-03 1992-10-16 Lille Transfusion Sanguine COMPOSITION FOR STABILIZING BLOOD PLASMA DURING PASTEURIZATION.
FR2687317B1 (en) * 1992-02-13 1995-06-23 Aetsrn COMPOSITION FOR STABILIZING BLOOD PLASMA DURING PASTEURIZATION AND PASTEURIZED PLASMATIC SOLUTION FOR THERAPEUTIC USE.
DE4342132C1 (en) * 1993-12-10 1994-11-03 Octapharma Ag Process for the preparation of virus-inactivated vitamin K-dependent plasma components, and protein C and protein S-containing compositions by membrane chromatography
GB0521139D0 (en) 2005-10-18 2005-11-23 Univ Sheffield Therapeutic agent

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4327086A (en) * 1980-03-27 1982-04-27 The Green Cross Corporation Process for heat treatment of aqueous solution containing human blood coagulation factor XIII

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4081432A (en) * 1977-07-25 1978-03-28 Monsanto Company Method of separating a Factor IX preparation from plasma using ethylene-maleic anhydride polymers
DE2916711A1 (en) * 1979-04-25 1980-11-06 Behringwerke Ag Blood coagulation factors and process for their manufacture

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4327086A (en) * 1980-03-27 1982-04-27 The Green Cross Corporation Process for heat treatment of aqueous solution containing human blood coagulation factor XIII

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4960757A (en) * 1982-08-19 1990-10-02 Behringwerke Aktiengesellschaft Pasteurized human fibrinogen (HF), a process for its preparation, and its use
US4562072A (en) * 1982-10-09 1985-12-31 Behringwerke Aktiengesellschaft Process for the pasteurization of antihemophilic cryoprecipitate (AHC) and antihemophilic cryoprecipitate prepared thereby
US4687664A (en) * 1983-05-02 1987-08-18 Immuno Aktiengesellschaft Fur Chemisch-Medizinische Produkte Method of inactivating reproducible pathogens
US4764369A (en) * 1983-07-14 1988-08-16 New York Blood Center Inc. Undenatured virus-free biologically active protein derivatives
US4820805A (en) * 1983-07-14 1989-04-11 New York Blood Center, Inc. Undenatured virus-free trialkyl phosphate treated biologically active protein derivatives
US4615886A (en) * 1983-08-31 1986-10-07 The United States Of America As Represented By The Secretary Of The Department Of Health & Human Services Utilizing a halohydrocarbon containing dissolved water to inactivate a lipid virus
US6346277B1 (en) * 1983-10-08 2002-02-12 Aventis Behring Gmbh Process for the pasteurization of plasma or concentrates of blood coagulation factors II, VII, IX and X
US4490361A (en) * 1983-12-02 1984-12-25 Alpha Therapeutic Corporation Virus inactivating heat treatment of plasma fractions
WO1985005273A1 (en) * 1984-05-18 1985-12-05 Purcell Robert H Utilizing a halohydrocarbon containing dissolved water to inactivate a lipid virus
AU592757B2 (en) * 1984-05-18 1990-01-25 Stephen M. Feinstone Utilizing a halohydrocarbon containing dissolved water to inactivate a lipid virus
US5171569A (en) * 1985-03-15 1992-12-15 National Research Development Corporation Factor IX preparations uncontaminated by plasma components or pox virus
US4876241A (en) * 1987-05-22 1989-10-24 Armour Pharmaceutical Company Stabilization of biological and pharmaceutical products during thermal inactivation of viral and bacterial contaminants
WO1989005652A1 (en) * 1987-12-21 1989-06-29 American National Red Cross Pure factor ix product
US6280729B1 (en) 1991-03-01 2001-08-28 Aventis Behring Llc Preparation of factor IX
WO1992015324A1 (en) * 1991-03-01 1992-09-17 Rhone-Poulenc Rorer International (Holdings) Inc. Preparation of factor ix
US6043215A (en) * 1991-03-01 2000-03-28 Aventis Behring L.L.C. Preparation of factor IX
US5864016A (en) * 1991-06-20 1999-01-26 Immuno Aktiengesellschaft Blood product, a method of producing the same and a method of determining the virus inactivation capacity of an inactivation treatment
US5614405A (en) * 1991-06-20 1997-03-25 Immuno Aktiengesellschaft Method of determining the virus inactivation capacity of an inactivation treatment
US5410022A (en) * 1992-04-24 1995-04-25 Immuno Aktiengesellschaft Method of producing a factor VIII preparation
US5733885A (en) * 1992-12-16 1998-03-31 Immuno Aktiengesellschaft Method of producing a virus-safe biological preparation
US5639730A (en) * 1992-12-16 1997-06-17 Immuno Aktiengesellschaft Method of producing a virus-safe biological preparation
US5614493A (en) * 1993-06-18 1997-03-25 Immuno Ag Use of human protein C for prevention and treatment of depositions of thrombocytes
US6372716B1 (en) * 1994-04-26 2002-04-16 Genetics Institute, Inc. Formulations for factor IX
US5770700A (en) * 1996-01-25 1998-06-23 Genetics Institute, Inc. Liquid factor IX formulations
EP1010852A1 (en) 1998-12-15 2000-06-21 Schlegel BVBA Sealing gasket and method of making and inserting the same

Also Published As

Publication number Publication date
DE3168834D1 (en) 1985-03-21
DE3045153A1 (en) 1982-07-08
IL64396A0 (en) 1982-02-28
ES8206975A1 (en) 1982-09-01
EP0053338A2 (en) 1982-06-09
AU544157B2 (en) 1985-05-16
CA1182047A (en) 1985-02-05
JPH0348171B2 (en) 1991-07-23
ATE11640T1 (en) 1985-02-15
JPS57120524A (en) 1982-07-27
EP0053338A3 (en) 1982-08-04
IL64396A (en) 1985-02-28
EP0053338B1 (en) 1985-02-06
AU7795081A (en) 1982-06-10
MX6947E (en) 1986-12-19
ES507400A0 (en) 1982-09-01

Similar Documents

Publication Publication Date Title
US4405603A (en) Method for rendering factors IX and X hepatitis-safe with calcium ions
US4404187A (en) Method for rendering factors II and VII hepatitis-safe with a chelating agent
CA1126652A (en) Antithrombin preparation and process for the production thereof
US4327086A (en) Process for heat treatment of aqueous solution containing human blood coagulation factor XIII
US5457181A (en) Preparation of a high-purity human factor IX concentrate and other plasmatic proteins and their therapeutic use
US4297344A (en) Blood coagulation factors and process for their manufacture
KR0149999B1 (en) Pasteurised purified von willebrand factor concentrate, and method of its prepartion
JPH05186369A (en) Method for producing concentrated human thrombin liquid for therapeutic application
US4562072A (en) Process for the pasteurization of antihemophilic cryoprecipitate (AHC) and antihemophilic cryoprecipitate prepared thereby
US4379085A (en) Heat stabilization of plasma proteins
FI81363B (en) FOERFARANDE FOER PASTOERISERING AV PREPARAT AV BLODKOAGULERINGSFAKTORERNA II, VII, IX OCH X.
KR960007922B1 (en) Process for the preparation of pp4 for the pasteurization
US4442213A (en) Process for the preparation of plasminogen and plasminogen thus prepared
US6063909A (en) Preparation of factor IX
AU658238B2 (en) A process for the production of a virus-free concentrate of thrombin
US5043428A (en) Pasteurized, isoagglutinin-free factor VIII preparation and a process for its production
CA1182748A (en) Method for synthesizing procoagulant factor viii activity
JPS61189228A (en) Production of blood coagulation factor viii
US5286849A (en) Purification of factor IX
EP0401232B1 (en) A process for pasteurization of aqueous solutions of factor viii
JPH0530812B2 (en)
AU665452C (en) Purification of factor IX
JPS6348220A (en) Production of blood-coagulating factor ix complex
JPS6351336A (en) Manufacture of vitamin k dependent coagulation factor medicine containing low prothrombin content

Legal Events

Date Code Title Description
AS Assignment

Owner name: BEHRINGWERKE AKTIENGESELLSCHAFT, MARBURG/LAHN, GER

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:SCHWINN, HORST;HEIMBURGER, NORBERT;KUMPE, GERHARDT;AND OTHERS;REEL/FRAME:004115/0752

Effective date: 19811112

STCF Information on status: patent grant

Free format text: PATENTED CASE

FEPP Fee payment procedure

Free format text: PAYER NUMBER DE-ASSIGNED (ORIGINAL EVENT CODE: RMPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 4TH YEAR, PL 96-517 (ORIGINAL EVENT CODE: M170); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 4

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 8TH YEAR, PL 96-517 (ORIGINAL EVENT CODE: M171); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 8

FEPP Fee payment procedure

Free format text: SURCHARGE FOR LATE PAYMENT, LARGE ENTITY (ORIGINAL EVENT CODE: M186); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

MAFP Maintenance fee payment

Free format text: PAYMENT OF MAINTENANCE FEE, 12TH YEAR, LARGE ENTITY (ORIGINAL EVENT CODE: M185); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Year of fee payment: 12

FEPP Fee payment procedure

Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

Free format text: PAYER NUMBER DE-ASSIGNED (ORIGINAL EVENT CODE: RMPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY

AS Assignment

Owner name: HOECHST AKTIENGESELLSCHAFT, GERMANY

Free format text: MERGER;ASSIGNOR:BERHINGWERKE GMBH;REEL/FRAME:009445/0161

Effective date: 19961122

Owner name: CENTEON PHARMA GMBH, GERMANY

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:HOECHST AKTIENGESELLSCHAFT;REEL/FRAME:009027/0911

Effective date: 19970801